CN107794593A - Thermoplastic cellulose and aliphatic aromatic polyester blending fibres and preparation method - Google Patents
Thermoplastic cellulose and aliphatic aromatic polyester blending fibres and preparation method Download PDFInfo
- Publication number
- CN107794593A CN107794593A CN201610803924.4A CN201610803924A CN107794593A CN 107794593 A CN107794593 A CN 107794593A CN 201610803924 A CN201610803924 A CN 201610803924A CN 107794593 A CN107794593 A CN 107794593A
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- CN
- China
- Prior art keywords
- cellulose
- acid
- aliphatic aromatic
- aliphatic
- thermoplastic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 229920002678 cellulose Polymers 0.000 title claims abstract description 157
- 239000001913 cellulose Substances 0.000 title claims abstract description 124
- 238000002156 mixing Methods 0.000 title claims abstract description 99
- 229920001169 thermoplastic Polymers 0.000 title claims abstract description 97
- 239000004416 thermosoftening plastic Substances 0.000 title claims abstract description 97
- 229920000728 polyester Polymers 0.000 title claims description 21
- 238000002360 preparation method Methods 0.000 title description 9
- 239000000203 mixture Substances 0.000 claims abstract description 150
- 229920001634 Copolyester Polymers 0.000 claims abstract description 86
- 239000000463 material Substances 0.000 claims abstract description 59
- 239000000835 fiber Substances 0.000 claims abstract description 50
- 238000000034 method Methods 0.000 claims abstract description 46
- 230000000977 initiatory effect Effects 0.000 claims abstract description 41
- 238000001125 extrusion Methods 0.000 claims abstract description 37
- 239000000155 melt Substances 0.000 claims abstract description 29
- 230000004927 fusion Effects 0.000 claims abstract description 9
- 239000002245 particle Substances 0.000 claims description 122
- 229920006217 cellulose acetate butyrate Polymers 0.000 claims description 51
- -1 valerate ester Chemical class 0.000 claims description 35
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 23
- 239000002994 raw material Substances 0.000 claims description 22
- 125000003118 aryl group Chemical group 0.000 claims description 20
- 238000001816 cooling Methods 0.000 claims description 19
- 125000001931 aliphatic group Chemical group 0.000 claims description 18
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 claims description 18
- 239000002253 acid Substances 0.000 claims description 11
- 150000002148 esters Chemical class 0.000 claims description 11
- 238000006467 substitution reaction Methods 0.000 claims description 10
- 238000002844 melting Methods 0.000 claims description 9
- 230000008018 melting Effects 0.000 claims description 9
- 235000019260 propionic acid Nutrition 0.000 claims description 9
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 claims description 9
- PUPZLCDOIYMWBV-UHFFFAOYSA-N (+/-)-1,3-Butanediol Chemical compound CC(O)CCO PUPZLCDOIYMWBV-UHFFFAOYSA-N 0.000 claims description 4
- 150000007524 organic acids Chemical class 0.000 claims description 4
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Natural products CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 claims description 3
- 125000001424 substituent group Chemical group 0.000 claims description 3
- 229940070710 valerate Drugs 0.000 claims description 3
- PUJRSOVINMPNIQ-UHFFFAOYSA-N acetic acid;decanoic acid Chemical compound CC(O)=O.CCCCCCCCCC(O)=O PUJRSOVINMPNIQ-UHFFFAOYSA-N 0.000 claims description 2
- IIOPVJIGEATDBS-UHFFFAOYSA-N acetic acid;dodecanoic acid Chemical compound CC(O)=O.CCCCCCCCCCCC(O)=O IIOPVJIGEATDBS-UHFFFAOYSA-N 0.000 claims description 2
- ZGJVTOHMNLDNNU-UHFFFAOYSA-N acetic acid;heptanoic acid Chemical compound CC(O)=O.CCCCCCC(O)=O ZGJVTOHMNLDNNU-UHFFFAOYSA-N 0.000 claims description 2
- YQAHABBBFVAGBK-UHFFFAOYSA-N acetic acid;hexadecanoic acid Chemical compound CC(O)=O.CCCCCCCCCCCCCCCC(O)=O YQAHABBBFVAGBK-UHFFFAOYSA-N 0.000 claims description 2
- 125000004432 carbon atom Chemical group C* 0.000 claims description 2
- POULHZVOKOAJMA-UHFFFAOYSA-M dodecanoate Chemical compound CCCCCCCCCCCC([O-])=O POULHZVOKOAJMA-UHFFFAOYSA-M 0.000 claims description 2
- UFCZCJYLUGMEJH-UHFFFAOYSA-N dodecanoic acid;propanoic acid Chemical compound CCC(O)=O.CCCCCCCCCCCC(O)=O UFCZCJYLUGMEJH-UHFFFAOYSA-N 0.000 claims description 2
- LYBHQLWKGWZMPP-UHFFFAOYSA-N heptanoic acid propanoic acid Chemical compound CCC(O)=O.CCCCCCC(O)=O LYBHQLWKGWZMPP-UHFFFAOYSA-N 0.000 claims description 2
- CUNOVGHBBXMFLM-UHFFFAOYSA-N hexadecanoic acid;propanoic acid Chemical compound CCC(O)=O.CCCCCCCCCCCCCCCC(O)=O CUNOVGHBBXMFLM-UHFFFAOYSA-N 0.000 claims description 2
- 229940070765 laurate Drugs 0.000 claims description 2
- CUFMJUIUCGVLMS-UHFFFAOYSA-N octanoic acid;propanoic acid Chemical compound CCC(O)=O.CCCCCCCC(O)=O CUFMJUIUCGVLMS-UHFFFAOYSA-N 0.000 claims description 2
- 235000005985 organic acids Nutrition 0.000 claims description 2
- DQEFEBPAPFSJLV-UHFFFAOYSA-N Cellulose propionate Chemical compound CCC(=O)OCC1OC(OC(=O)CC)C(OC(=O)CC)C(OC(=O)CC)C1OC1C(OC(=O)CC)C(OC(=O)CC)C(OC(=O)CC)C(COC(=O)CC)O1 DQEFEBPAPFSJLV-UHFFFAOYSA-N 0.000 claims 1
- 125000004429 atom Chemical group 0.000 claims 1
- 229920006218 cellulose propionate Polymers 0.000 claims 1
- 238000009833 condensation Methods 0.000 claims 1
- 230000005494 condensation Effects 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 230000008569 process Effects 0.000 abstract description 9
- 235000010980 cellulose Nutrition 0.000 description 95
- 229920001896 polybutyrate Polymers 0.000 description 62
- 239000000843 powder Substances 0.000 description 25
- 238000005453 pelletization Methods 0.000 description 23
- 229920008347 Cellulose acetate propionate Polymers 0.000 description 20
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 20
- 238000012360 testing method Methods 0.000 description 20
- 230000000052 comparative effect Effects 0.000 description 19
- 229910052799 carbon Inorganic materials 0.000 description 14
- 230000000694 effects Effects 0.000 description 13
- 230000008859 change Effects 0.000 description 12
- 238000005538 encapsulation Methods 0.000 description 12
- 229920000642 polymer Polymers 0.000 description 12
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 10
- 238000001291 vacuum drying Methods 0.000 description 10
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 9
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 9
- 238000004364 calculation method Methods 0.000 description 9
- 239000003795 chemical substances by application Substances 0.000 description 9
- 230000009477 glass transition Effects 0.000 description 9
- 150000008065 acid anhydrides Chemical class 0.000 description 8
- 238000002425 crystallisation Methods 0.000 description 7
- 230000008025 crystallization Effects 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 7
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 7
- KDYFGRWQOYBRFD-UHFFFAOYSA-N succinic acid Chemical compound OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 238000005259 measurement Methods 0.000 description 6
- 238000012545 processing Methods 0.000 description 6
- 238000009987 spinning Methods 0.000 description 6
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 5
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 5
- 230000000875 corresponding effect Effects 0.000 description 5
- 229960005137 succinic acid Drugs 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 241000607479 Yersinia pestis Species 0.000 description 4
- 235000011037 adipic acid Nutrition 0.000 description 4
- 125000000217 alkyl group Chemical group 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 4
- 238000000576 coating method Methods 0.000 description 4
- 239000003205 fragrance Substances 0.000 description 4
- 239000003292 glue Substances 0.000 description 4
- DNIAPMSPPWPWGF-UHFFFAOYSA-N monopropylene glycol Natural products CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000001384 succinic acid Substances 0.000 description 4
- 230000002195 synergetic effect Effects 0.000 description 4
- 239000004970 Chain extender Substances 0.000 description 3
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 3
- 229920000297 Rayon Polymers 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 3
- 239000012298 atmosphere Substances 0.000 description 3
- UJMDYLWCYJJYMO-UHFFFAOYSA-N benzene-1,2,3-tricarboxylic acid Chemical class OC(=O)C1=CC=CC(C(O)=O)=C1C(O)=O UJMDYLWCYJJYMO-UHFFFAOYSA-N 0.000 description 3
- 229920000229 biodegradable polyester Polymers 0.000 description 3
- 239000004622 biodegradable polyester Substances 0.000 description 3
- 239000000112 cooling gas Substances 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 3
- 230000003993 interaction Effects 0.000 description 3
- 239000011159 matrix material Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 239000004745 nonwoven fabric Substances 0.000 description 3
- 229920002959 polymer blend Polymers 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000002411 thermogravimetry Methods 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- 229920000562 Poly(ethylene adipate) Polymers 0.000 description 2
- TYFQFVWCELRYAO-UHFFFAOYSA-N Suberic acid Natural products OC(=O)CCCCCCC(O)=O TYFQFVWCELRYAO-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 239000001361 adipic acid Substances 0.000 description 2
- 125000002723 alicyclic group Chemical group 0.000 description 2
- 150000007933 aliphatic carboxylic acids Chemical class 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 2
- 230000003078 antioxidant effect Effects 0.000 description 2
- 238000003556 assay Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- QMKYBPDZANOJGF-UHFFFAOYSA-N benzene-1,3,5-tricarboxylic acid Chemical compound OC(=O)C1=CC(C(O)=O)=CC(C(O)=O)=C1 QMKYBPDZANOJGF-UHFFFAOYSA-N 0.000 description 2
- 239000012620 biological material Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 150000001721 carbon Chemical group 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 229920003086 cellulose ether Polymers 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical compound O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 description 2
- 230000001965 increasing effect Effects 0.000 description 2
- 239000011256 inorganic filler Substances 0.000 description 2
- 229910003475 inorganic filler Inorganic materials 0.000 description 2
- 230000016507 interphase Effects 0.000 description 2
- 239000012948 isocyanate Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- UFWIBTONFRDIAS-UHFFFAOYSA-N naphthalene-acid Natural products C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- 229920005615 natural polymer Polymers 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 235000006408 oxalic acid Nutrition 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000003672 processing method Methods 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- KUCOHFSKRZZVRO-UHFFFAOYSA-N terephthalaldehyde Chemical compound O=CC1=CC=C(C=O)C=C1 KUCOHFSKRZZVRO-UHFFFAOYSA-N 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- 239000004753 textile Substances 0.000 description 2
- VXUYXOFXAQZZMF-UHFFFAOYSA-N titanium(IV) isopropoxide Chemical compound CC(C)O[Ti](OC(C)C)(OC(C)C)OC(C)C VXUYXOFXAQZZMF-UHFFFAOYSA-N 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- ZWVMLYRJXORSEP-UHFFFAOYSA-N 1,2,6-Hexanetriol Chemical class OCCCCC(O)CO ZWVMLYRJXORSEP-UHFFFAOYSA-N 0.000 description 1
- UNVGBIALRHLALK-UHFFFAOYSA-N 1,5-Hexanediol Chemical class CC(O)CCCCO UNVGBIALRHLALK-UHFFFAOYSA-N 0.000 description 1
- ALVZNPYWJMLXKV-UHFFFAOYSA-N 1,9-Nonanediol Chemical class OCCCCCCCCCO ALVZNPYWJMLXKV-UHFFFAOYSA-N 0.000 description 1
- BRBMYNGGGPTKKL-UHFFFAOYSA-N 1,9-decanediol Chemical class CC(O)CCCCCCCCO BRBMYNGGGPTKKL-UHFFFAOYSA-N 0.000 description 1
- RTBFRGCFXZNCOE-UHFFFAOYSA-N 1-methylsulfonylpiperidin-4-one Chemical compound CS(=O)(=O)N1CCC(=O)CC1 RTBFRGCFXZNCOE-UHFFFAOYSA-N 0.000 description 1
- AXPZIVKEZRHGAS-UHFFFAOYSA-N 3-benzyl-5-[(2-nitrophenoxy)methyl]oxolan-2-one Chemical compound [O-][N+](=O)C1=CC=CC=C1OCC1OC(=O)C(CC=2C=CC=CC=2)C1 AXPZIVKEZRHGAS-UHFFFAOYSA-N 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- 229920000298 Cellophane Polymers 0.000 description 1
- 229920002101 Chitin Polymers 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- WLJVNTCWHIRURA-UHFFFAOYSA-N Heptanedioic acid Natural products OC(=O)CCCCCC(O)=O WLJVNTCWHIRURA-UHFFFAOYSA-N 0.000 description 1
- 239000005057 Hexamethylene diisocyanate Substances 0.000 description 1
- OWIKHYCFFJSOEH-UHFFFAOYSA-N Isocyanic acid Chemical compound N=C=O OWIKHYCFFJSOEH-UHFFFAOYSA-N 0.000 description 1
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- BDJRBEYXGGNYIS-UHFFFAOYSA-N Nonanedioid acid Natural products OC(=O)CCCCCCCC(O)=O BDJRBEYXGGNYIS-UHFFFAOYSA-N 0.000 description 1
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- 229920001273 Polyhydroxy acid Polymers 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 241001464837 Viridiplantae Species 0.000 description 1
- ASRPLWIDQZYBQK-UHFFFAOYSA-N acetic acid;pentanoic acid Chemical compound CC(O)=O.CCCCC(O)=O ASRPLWIDQZYBQK-UHFFFAOYSA-N 0.000 description 1
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- XLJMAIOERFSOGZ-UHFFFAOYSA-N anhydrous cyanic acid Natural products OC#N XLJMAIOERFSOGZ-UHFFFAOYSA-N 0.000 description 1
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- HTXVEEVTGGCUNC-UHFFFAOYSA-N heptane-1,3-diol Chemical class CCCCC(O)CCO HTXVEEVTGGCUNC-UHFFFAOYSA-N 0.000 description 1
- NNYOSLMHXUVJJH-UHFFFAOYSA-N heptane-1,5-diol Chemical class CCC(O)CCCCO NNYOSLMHXUVJJH-UHFFFAOYSA-N 0.000 description 1
- UQGLNXPQGUMNRU-UHFFFAOYSA-N heptane-1,6-diol Chemical class CC(O)CCCCCO UQGLNXPQGUMNRU-UHFFFAOYSA-N 0.000 description 1
- SXCBDZAEHILGLM-UHFFFAOYSA-N heptane-1,7-diol Chemical class OCCCCCCCO SXCBDZAEHILGLM-UHFFFAOYSA-N 0.000 description 1
- 125000004836 hexamethylene group Chemical group [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 1
- AVIYEYCFMVPYST-UHFFFAOYSA-N hexane-1,3-diol Chemical class CCCC(O)CCO AVIYEYCFMVPYST-UHFFFAOYSA-N 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical class OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- 229940051250 hexylene glycol Drugs 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 239000010977 jade Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000000048 melt cooling Methods 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- LJZULWUXNKDPCG-UHFFFAOYSA-N nonane-1,2-diol Chemical class CCCCCCCC(O)CO LJZULWUXNKDPCG-UHFFFAOYSA-N 0.000 description 1
- CGNJFUJNEYIYRZ-UHFFFAOYSA-N nonane-1,3-diol Chemical class CCCCCCC(O)CCO CGNJFUJNEYIYRZ-UHFFFAOYSA-N 0.000 description 1
- UOELQPIRLNNPNZ-UHFFFAOYSA-N nonane-1,6-diol Chemical class CCCC(O)CCCCCO UOELQPIRLNNPNZ-UHFFFAOYSA-N 0.000 description 1
- HGQPJWDYHDWFEH-UHFFFAOYSA-N nonane-1,7-diol Chemical class CCC(O)CCCCCCO HGQPJWDYHDWFEH-UHFFFAOYSA-N 0.000 description 1
- WBSRHBNFOLDTGU-UHFFFAOYSA-N nonane-1,8-diol Chemical class CC(O)CCCCCCCO WBSRHBNFOLDTGU-UHFFFAOYSA-N 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000011087 paperboard Substances 0.000 description 1
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
- WCVRQHFDJLLWFE-UHFFFAOYSA-N pentane-1,2-diol Chemical compound CCCC(O)CO WCVRQHFDJLLWFE-UHFFFAOYSA-N 0.000 description 1
- RUOPINZRYMFPBF-UHFFFAOYSA-N pentane-1,3-diol Chemical class CCC(O)CCO RUOPINZRYMFPBF-UHFFFAOYSA-N 0.000 description 1
- 230000029553 photosynthesis Effects 0.000 description 1
- 238000010672 photosynthesis Methods 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000002964 rayon Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000004627 regenerated cellulose Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 238000000518 rheometry Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 229940032021 tetramune Drugs 0.000 description 1
- 238000001757 thermogravimetry curve Methods 0.000 description 1
- 150000003608 titanium Chemical class 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- ARCGXLSVLAOJQL-UHFFFAOYSA-N trimellitic acid Chemical class OC(=O)C1=CC=C(C(O)=O)C(C(O)=O)=C1 ARCGXLSVLAOJQL-UHFFFAOYSA-N 0.000 description 1
- QXJQHYBHAIHNGG-UHFFFAOYSA-N trimethylolethane Chemical compound OCC(C)(CO)CO QXJQHYBHAIHNGG-UHFFFAOYSA-N 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
- 208000016261 weight loss Diseases 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
- D01F8/02—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from cellulose, cellulose derivatives, or proteins
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
- D01F8/04—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
- D01F8/14—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyester as constituent
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Artificial Filaments (AREA)
Abstract
The present invention relates to the blend fibers of a kind of thermoplastic cellulose and aliphatic aromatic copolyesters, and viscosity is high during mainly solving thermoplastic cellulose low temperature process in the prior art, and fibre forming property is poor, and makes the limited technical problem of its application field.The blend that the present invention forms by using the aliphatic aromatic copolyesters of the thermoplastic cellulose by 20% to 80% quality and 80% to 20% quality, the blend is prepared by a kind of continuous fusion extrusion blending method, and the blending addition theoretical value of the melt viscosity of blend than two kinds of initiation materials under the conditions of low shear rate is at least low by about 20%；The technical scheme at least lower by 20% than the blending addition theoretical value of two kinds of initiation materials, preferably solves the problem, available in the industrialized production of thermoplastic cellulose and the blend fibers of aliphatic aromatic copolyesters under the conditions of high-rate of shear.
Description
Technical field
The invention belongs to the blend material field of thermoplastic cellulose and aliphatic aromatic copolyesters, Ju Ti Wataru and one
The blend fibers of kind of thermoplastic cellulose and aliphatic aromatic copolyesters with the special rheological equationm of state, this invention and also Wataru and
A kind of thermoplastic cellulose prepared with the special rheological equationm of state and aliphatic aromatic polyester blending fibres and non-woven fabrics
Method.
Technical background
Cellulose is the organic polymer that reserves are most on the earth, and the most biological material of annual reproducible amounts.
Cellulose is the structural material in non-green plant cell wall, and xylophyta contains about 30-40% cellulose, cotton fiber then contains
There is about 90% cellulose.The major commercial use of cellulose is paper and cardboard, separately have a small amount of cellulose be used for prepare as match
The regenerated celluloses such as fine jade phenol (Cellophane), viscose glue (Rayon) and some fibre element derivative.
Because cellulose is the natural polymer that plant changes into the carbon dioxide in air and water by photosynthesis,
Therefore the carbon in cellulose belong to fixed in the recent period carbon and different from fossil fuel and its petroleum chemicals such as oil or coals
In millions of years before fixed carbon, the carbon that different times are fixed can pass through14C isotope standardizations are examined
Survey.Due to these difference, had based on bio-based high molecular products prepared by biomass material relative to petroleum base high molecular products
There is the advantage of raw material low-carbon, then using low energy consumption and the production technology of low-carbon emission, it is possible to produce the high score of green low-carbon
Sub- product.For such consideration, natural polymer, including cellulose, hemicellulose, lignin, starch, chitin etc., and its
Derivative Tetramune receives increasingly increased concern and research and development in the whole world, to develop high-quality green low-carbon environment-friendly product.And
The extensive use of the green low-carbon product of (Life Cycle Assessment) confirmation is assessed by Life Cycles, it will help
Green production and Green Lifestyle are supported, to reduce the content of the greenhouse gases (carbon dioxide etc.) in air and alleviation
The climate change in the whole world contributes.
Although cellulose has the low-carbon advantage on raw material, make spinning application cellulose amount it is seldom, this is due to fibre
The heat decomposition temperature of dimension element is less than its fusing point without thermoplastic properties.To overcome this defect of cellulose, researcher opens
The regenerated cellulose of solwution method production is have issued, i.e., cellulose or cellulose derivative are first dissolved in solvent, by solution
Machine-shaping, it is changed into cellulose again after being prepared into film or spinning, the viscose rayon in textile industry is i.e. in this way
Prepare.
In addition for cellulose derivative when three hydroxyls that each of which is repeated on glucose unit turn through enough chemistry
After change, can also have relatively low fusing or plasticization temperature, limited thermoplastic processing can be carried out, turn into thermoplastic cellulose, this
Class material includes the cellulose esters and cellulose ether of certain substitution value.Due to the yield and product category of this kind of cellulose derivative
It is limited, and the ratio of viscosities of industrialized such product is higher, is especially apparent under compared with low processing temperature, is not suitable for needing low melt
The processing method of viscosity such as spinning, injection etc.；Cellulose esters and cellulose ether, which have, at present is greatly used as coating or gluing
The additive in agent field【High Zhenhua, Di Mingwei,《Biological material and application》, 2008】.Therefore, from the angle of processed and applied,
There are exploitation low viscosity and the technical need of the thermoplastic cellulose derivative with excellent machinability, to meet related raw material
The market demand.
So far, there has been no reported in literature thermoplastic cellulose and the special flow of aliphatic aromatic copolyester blends
Change behavior, and effectively reduce thermoplastic cellulose and aliphatic aromatic copolyester blends without offer in the prior art
The method of melt viscosity, it is restricted the application of this kind of blend.
The invention discloses a kind of thermoplastic cellulose that effectively reduces to glue with aliphatic aromatic copolyester blends melt
The continuous fusion extrusion method of degree, it was found that unexpected phenomenon and result, disclose the blending with the special rheological equationm of state
Thing is formed, and the blend successfully has been applied into fiber and non-woven fabrics field.
The content of the invention
Present invention solves the technical problem that one of be thermoplastic cellulose and aliphatic aromatic copolyesters in the prior art
Blend melt viscosity is too high and the problem of may not apply to need the blend fibers of low melt viscosity, there is provided a kind of thermoplasticity
Cellulose and aliphatic aromatic polyester blending fibres, the thermoplastic cellulose and aliphatic aromatic copolyester blends
With the special rheological equationm of state, the viscosity " unexpected " of blend effectively can be fallen below thermoplastic fibres element and fat
The blending addition theoretical viscosity of race's aromatic copolyester initiation material；So that the blend has realizes preparation at a lower temperature
Into the processing characteristics of fiber, obtained fiber is better than the similar blend fibers of prior art, and due to blend melt viscosity
It is low, it can be made more to save in process.
It is fine that the two of the technical problems to be solved by the invention are to provide a kind of thermoplasticity prepared with the special rheological equationm of state
Dimension element and the method for aliphatic aromatic polyester blending fibres, the melt viscosity for the blend that this method obtains is in low sheraing
Blending addition theoretical value under rate conditions than two kinds of initiation materials is at least low by about 20%；Two kinds of the ratio under the conditions of high-rate of shear
The blending addition theoretical value at least low 20% of initiation material.
One of in order to solve the above-mentioned technical problem, the technical solution adopted in the present invention is：One kind has special rheological characteristic
The thermoplastic cellulose of matter and aliphatic aromatic polyester blending fibres, the blend fibers contain 20% to 80% quality
Thermoplastic cellulose and 80% to 20% quality aliphatic aromatic copolyesters, wherein, the thermoplastic fibre of the quality
The melt viscosity of element and aliphatic aromatic copolyester blends compares the blending of two kinds of initiation materials under the conditions of low shear rate
Addition theoretical value at least low about 20%；Compare the blending addition theoretical value raw material of two kinds of initiation materials extremely under the conditions of high-rate of shear
Few low 20%；Wherein, the thermoplastic cellulose is selected from the cellulose esters that cellulose and at least two organic acids are formed, described to have
The total number of carbon atoms of machine acid is more than or equal to 6.
In above-mentioned technical proposal, described " low shear rate " refers to that shear rate is 100s-1；Described " high shear speed
Rate " refers to 1000s-1Or 1363s-1。
In above-mentioned technical proposal, the substitution value of described thermoplastic cellulose is preferably greater than 1.0；The cellulose being more suitable for spreads out
The substitution value of biology is more than 1.5；The substitution value of particularly suitable cellulose derivative is more than 2.0.
In above-mentioned technical proposal, described thermoplastic cellulose is preferably cellulose acetate-butyrate, acetic acid valeric acid fiber
Plain ester, acetic acid cellulose caproate ester, acetic acid enanthic acid cellulose esters, laurate cellulose esters, acetic acid cellulose pelargonate ester, acetic acid
Capric acid cellulose esters, acetic acid laurate cellulose esters, acetic acid palmitic acid cellulose esters, acetic acid cellulose stearate ester, propionic acid fourth
Acid cellulose ester, propionic acid cellulose valerate ester, propionic acid cellulose caproate ester, propionic acid enanthic acid cellulose esters, propionic acid octanoic acid cellulose
Ester, propionic acid cellulose pelargonate ester, propionic acid capric acid cellulose esters, propionic acid laurate cellulose esters, propionic acid palmitic acid cellulose esters, third
Sour cellulose stearate ester etc..
In above-mentioned technical proposal, described aliphatic aromatic copolyesters is preferably α, ω-aliphatic diacid and aromatic series
The copolyesters that diacid or derivatives thereof is condensed with aliphatic diol；Described aliphatic diacid is preferably to contain 2 to 22 masters
The α of chain carbon atom, ω-aliphatic diacid, including：Oxalic acid, 1,3- malonic acid, butanedioic acid (1, 4- succinic acid), glutaric acid (1,5- penta
Diacid), adipic acid (1,6- adipic acid), 1,7- pimelic acid, 1,8- suberic acid, 1,9- azelaic acid, 1,10- decanedioic acid is until carbon atom
Number reaches 22 binary acid；The derivative of the aliphatic diacid includes acid anhydrides, ester, carboxylic acid halides of the preparation of above-mentioned diacid etc..
In above-mentioned technical proposal, described aliphatic diacid is preferably the aliphatic diacid containing substituent；Described substitution
Base is preferably straight chained alkyl, the alkyl with side chain, ring-like alkyl, the alkyl with unsaturated structure；With with other substitutions
The binary acid of base such as cyclohexyl.
In above-mentioned technical proposal, described aromatic diacid is preferably terephthalic acid (TPA), Isosorbide-5-Nitrae-naphthalene diacid, 2,7- naphthalenes two
Acid, 2,6- naphthalene diacid, 2,7- naphthalene diacid, 4,4 '-diphenyl ether diacid, 4,3 '-diphenyl ether diacid, 4,4 '-diphenyl sulfide diacid, 4,
3 '-diphenyl sulfide diacid, 4,4 '-diphenyl sulphone (DPS) diacid, 4,3 '-diphenyl sulphone (DPS) diacid, 4,4 '-benzophenone diacid, 4,3 '-hexichol first
At least one of diacid such as keto-dibasic acid；The derivative of described aromatic diacid preferably be selected from acid anhydrides prepared by above-mentioned diacid, ester,
At least one of carboxylic acid halides etc..
In above-mentioned technical proposal, the combination of described aliphatic diacid and aromatic diacid includes at least one above-mentioned fat
Race's diacid or aliphatic diacid derivative and at least one above-mentioned aromatic diacid or aromatic diacid derivative.Fitted in the present invention
Aliphatic diol for preparing aliphatic aromatic copolyesters includes ethylene glycol, 1,2-PD, 1,3-PD, 1,2- fourth
Glycol, 1,3-BDO, BDO, 1,2- pentanediol, 1,3- pentanediols, Isosorbide-5-Nitrae-pentanediol, 1,5-PD, 1,2- oneself
Glycol, 1,3- hexylene glycols, Isosorbide-5-Nitrae-hexylene glycol, 1,5- hexylene glycols, 1,6- hexylene glycols, 1,2- heptandiols, 1,3- heptandiols, Isosorbide-5-Nitrae-heptan
Glycol, 1,5- heptandiols, 1,6- heptandiols, 1,7- heptandiols, 1,2- ethohexadiols, 1,3- ethohexadiols, Isosorbide-5-Nitrae-ethohexadiol, 1,5- are pungent
Glycol, 1,6- ethohexadiols, 1,7- ethohexadiols, 1,8- ethohexadiols, 1,2- nonanediols, 1,3- nonanediols, Isosorbide-5-Nitrae-nonanediol, 1,5- nonyls
Glycol, 1,6- nonanediols, 1,7- nonanediols, 1,8- nonanediols, 1,9- nonanediols, 1,2- decanediols, 1,3- decanediols, the Isosorbide-5-Nitrae-last of the ten Heavenly stems
Glycol, 1,5- decanediols, 1,6- decanediols, 1,7- decanediols, 1,8- decanediols, 1,9- decanediols, 1,10- decanediols are until carbon
Atomicity reaches 24 glycol and dihydric alcohol with other substituents such as cyclohexyl.
In above-mentioned technical proposal, described aliphatic aromatic copolyesters is preferably poly terephthalic acid-co- oxalic acid second two
Alcohol ester, poly terephthalic acid-co- malonic acid glycol esters, poly terephthalic acid-co- EGS ethylene glycol succinates, poly- terephthaldehyde
Acid-co- EGG ethylene glycol glutarates, poly terephthalic acid-co- ethylene glycol adipates, poly terephthalic acid-co- suberic acid second
Diol ester, poly terephthalic acid-co- oxalic acid propylene glycol esters, poly terephthalic acid-co- malonic acid propylene glycol esters, poly- terephthaldehyde
Acid-co- succinic acid propylene glycol ester, poly terephthalic acid-co- glutaric acids propylene glycol ester, poly terephthalic acid-co- adipic acids third
It is diol ester, poly terephthalic acid-co- suberic acids propylene glycol ester, poly terephthalic acid-co- decanedioic acid propylene glycol ester, poly- to benzene two
Formic acid-co- oxalic acid butanediol esters, poly terephthalic acid-co- malonic acid butanediol esters, poly terephthalic acid-co- succinic acid fourths
It is diol ester, poly terephthalic acid-co- glutaric acids butanediol ester, poly terephthalic acid-co- tetramethylene adipates, poly- to benzene two
Formic acid-co- suberic acids butanediol ester, poly terephthalic acid-co- oxalic acid hexylene glycol esters, poly terephthalic acid-co- malonic acid oneself
Diol ester, poly terephthalic acid-co- succinic acid hexylene glycols ester, poly terephthalic acid-co- glutaric acid hexylene glycols ester, gather to benzene two
At least one of formic acid-co- adipic acid hexylene glycols ester, poly terephthalic acid-co- suberic acid hexylene glycol esters etc..
In above-mentioned technical proposal, the thermoplastic cellulose is preferably cellulose acetate-butyrate, and thermoplasticity now is fine
Dimension element has synergistic function with aliphatic aromatic copolyesters, and both blends not only possess above-mentioned special rheological characteristic
Matter, it was found that cellulose acetate-butyrate possesses commonly uses thermoplastic cellulose (such as cellulose acetate, acetate propionate fiber than other
Element etc.) with more preferable compatibility during polyester blending, i.e., solve thermoplastic cellulose and aliphatic aromatic well and be copolymerized
The problem of compatibility of ester is poor, both compatibilities are good, can widen the use range of initiation material significantly, while special
The rheological equationm of state can reduce the energy consumption in material processing.
In above-mentioned technical proposal, the aliphatic aromatic copolyesters is preferably poly terephthalic acid-co- adipic acids fourth two
Alcohol ester (PBAT), poly terephthalic acid-co- ethylene glycol adipates (PEAT), poly terephthalic acid-co- succinic acid ethylene glycol
Ester (PEST) and poly terephthalic acid-co- succinic acid-butanediol esters (PBST).
In above-mentioned technical proposal, the blend material be most preferably 20% to 80% quality acetylbutyrylcellulose with
Poly terephthalic acid-co- tetramethylene adipates the blend or poly terephthalic acid-co- succinic acid of 80% to 20% quality
Butanediol ester, the blend rheological property and compatibility performance now obtained is optimal, the fiber of corresponding processing characteristics and formation
Performance is best.
In above-mentioned technical proposal, the number-average molecular weight of the blend material is preferably at least more than 20000g/mol, enters one
Step is preferably at least more than 40000g/mol；Weight average molecular weight is preferably at least more than 60000g/mol, further preferably at least above
80000g/mol。。
In above-mentioned technical proposal, the blend material further preferably contains compatibility agent, inorganic filler, antioxidant, lubrication
At least one of agent, colouring agent etc..
In above-mentioned technical proposal, the melt viscosity of described blend is preferably in low shear rate (100s-1) under the conditions of compare
The blending addition theoretical value of two kinds of initiation materials is at least low 30%, and (mass ratio of preferably copolyesters and thermoplastic cellulose is
65%:35% to 35%:It is 65%), further preferably at least low 35% that (mass ratio of preferably copolyesters and thermoplastic cellulose is
35%:65%).
In above-mentioned technical proposal, the melt viscosity of described blend is preferably in high-rate of shear (1000 or 1363s-1) bar
25% (the preferably mass ratio of copolyesters and thermoplastic cellulose at least lower than the blending addition theoretical value of two kinds of initiation materials under part
For 65%:35% to 20%:80%), further preferably at least low 30% (the preferably mass ratio of copolyesters and thermoplastic cellulose
For 35%:65% to 20%:80%).
In above-mentioned technical proposal, the melt index of described blend material is preferably than the blending addition of two kinds of initiation materials
Theoretical value is at least high by about 10%, more preferably at least high about 40% (the preferably mass ratio of copolyesters and thermoplastic cellulose
For 65%:35% to 20%:80%), more preferably at least high about 60% (the more preferably quality of copolyesters and thermoplastic cellulose
Than for 35%:65%).
Aliphatic aromatic copolyesters applied to the present invention can be from above-mentioned a variety of different aliphatic diacids, fragrance
Race's diacid is prepared with aliphatic diol by polymerisation.The catalyst of polymerization includes the chemical combination containing metallic tin, antimony, titanium etc.
Thing.Titanium series catalyst includes tetraisopropyl titanate, butyl titanate etc..Aliphatic aromatic copolyesters includes the fat by chain extension
Fat race aromatic copolyester, it is a variety of that there is compound or polymer with carboxyl or hydroxyl reaction activity may be used as chain extender,
As included the isocyanates such as toluene di-isocyanate(TDI) (TDI) containing two and above functional group, the isocyanic acid of hexa-methylene two
Ester (hexamethylene diisocyanate, HMDI).Applicable chain extender also includes the change containing multiple epoxy-functionals
Compound, such as BASF productions ADR-4368C,ADR-4368CS etc..The chain extension of the present invention
Agent mass content is 0.2 to 4%, and the chain extender mass content in some concrete embodiments is 0.5 to 3%.
Aliphatic aromatic copolyesters in the present invention includes the linear and copolyesters with side chain.Synthesis carries side chain
Copolyesters one or more branching agents are added in building-up process.Side chain agent is generally polynary with two or more carboxyl
Acid, the polyalcohol with two or more hydroxyl or polyhydroxy-acid etc..Applicable side chain agent includes glycerine, trimethylolethane, three
Hydroxymethyl-propane, BT, pentaerythrite, 1,2,6- hexanetriols, D-sorbite, 1,2,3 benzenetricarboxylic acids
(hemimellitic acid), 1,2,4- benzenetricarboxylic acids (triimellitic acid), 1,3,5- benzenetricarboxylic acid (trimesic
) and acid anhydrides etc. acid.
In order to solve the above-mentioned technical problem two, the technical solution adopted in the present invention is：One kind prepares above-mentioned technical side
The method of any described thermoplastic cellulose of case and aliphatic aromatic polyester blending fibres, will using melt blending
The desired amount of thermoplastic cellulose is uniformly mixed in the molten state with the desired amount of aliphatic aromatic copolyesters, by altogether
Mixed thing melt cooling, it is granulated；Blends particles are squeezed after plastifying, melting and measure on screw extruder by spinneret orifice again
Go out to form melt stream, described thermoplastic cellulose and aliphatic aromatic polyester blending is prepared through cooling down, stretching
Fibres.
In above-mentioned technical proposal, described thermoplastic cellulose and aliphatic aromatic copolyester blends melt blending side
Method is preferably twin-screw continuous extrusion method.
In above-mentioned technical proposal, described thermoplastic cellulose and aliphatic aromatic copolyester blends melt blending side
Method is preferably included thermoplastic cellulose powder by continuous extruding pelletization and then again with aliphatic aromatic copolyesters according to institute
Need ratio to be added to after being blended on a double screw extruder and carry out extruding pelletization.
In above-mentioned technical proposal, described thermoplastic cellulose and aliphatic aromatic copolyester blends melt blending side
Method is preferably included thermoplastic cellulose powder by continuous extruding pelletization and then again with aliphatic aromatic copolyesters according to institute
The feeding ratio needed is dosed on a double screw extruder respectively carries out extruding pelletization.
In above-mentioned technical proposal, described thermoplastic cellulose and aliphatic aromatic copolyester blends melt blending side
Method, which preferably includes according to certain feeding ratio to measure thermoplastic cellulose powder and aliphatic aromatic copolyesters respectively, to be added
Enter to carrying out extruding pelletization on a double screw extruder.
In above-mentioned technical proposal, described thermoplastic cellulose and aliphatic aromatic copolyester blends melt blending side
The screw speed of method is preferably 50rpm to 1500rpm.
In above-mentioned technical proposal, described thermoplastic cellulose and aliphatic aromatic copolyester blends melt blending side
The temperature of method is preferably 140 DEG C to 240 DEG C.
Material therefor of the present invention and preparation method are simply described below below：
1. thermoplastic cellulose
The thermoplastic cellulose of the present invention is the very wide cellulose derivative of a kind of scope, such cellulose derivative
Each three hydroxylic moieties repeated on glucose unit or all carried out being esterified or be etherified etc. the chemical modification of form.Table
The extent index for levying its modification is substitution value (Degree of Substitution), and it is defined as each repetition glucose unit
The mean number substituted in upper three hydroxyls, maximum are 3.0 (3 hydroxyls are all substituted), and minimum is 0 (pure fiber
Element).
The thermoplastic cellulose ester included in the present invention include cellulose and two kinds and two or more alicyclic organic aliphatic carboxylic acids,
The mixed cellulose ester that organic fatty race acid anhydrides and organic fatty race carboxylic acid halides are formed, different alicyclic organic aliphatic carboxylic acids, organic fatty
The carbon number difference of race's acid anhydrides and organic fatty race carboxylic acid halides is more than or equal to 1.
Cellulose esters is generally made by native cellulose and the reactions such as organic acid, acid anhydrides or acyl chlorides, the hydroxyl in cellulose
Substitution value is from 0.5 to 2.8.Applicable cellulose ester product includes the Eastman of Eastman Chemical of U.S. productionTMAcetic acid fourth
Acid cellulose ester CAB-171-15, CAB-321-0.1, CAB-381-0.1, CAB-381-0.5, CAB-381-20, CAB-485-
10, CAB-500-5, CAB-531-1 etc..Such as：Butyric acid composition containing 50% mass fraction, 2.8% mass in CAB-531-1
The acetate component of fraction, the hydroxyl moieties of 1.7% mass fraction, the viscosity measured according to the standards of ASTM 1343 are 5.6 pools.It is fine
Tie up plain ester has application in industries such as fiber, weaving, coating, thermoplastic film, food additives and pharmaceutical industries.In coating
Industry, coating effect can be improved after with the addition of cellulose esters, including：Hardness, mobility, planarization, transparency and glossiness
Deng.Cellulose acetate propionate ester (CAP) and cellulose acetate-butyrate (CAB) are two kinds of wider cellulose mixtures of commercial use
Ester.
2. aliphatic aromatic copolyesters
The present invention aliphatic aromatic copolyesters be a kind of biodegradable plastic, by one or more aliphatic diols with
At least one aliphatic diacid or aliphatic diacid acid anhydride, the carboxylic acid halides of aliphatic two, the acyl ester of aliphatic two, also at least one aromatic series
Diacid or aromatic diacid acid anhydride, the carboxylic acid halides of aromatic series two, the acyl ester of aromatic series two, condensation polymerization obtain.
3. thermoplastic cellulose and biodegradable aliphatic aromatic copolyester blends
The blend that the present invention announces is by a kind of thermoplastic cellulose and a kind of biodegradable aliphatic aromatic
Copolyesters forms, and the wherein mass content of thermoplastic cellulose is 20% to 80%, biodegradable aliphatic aromatic copolyester
The mass content of ester is 80% to 20%.The blend is in addition to comprising composition described above, in addition to following at least one additive：
Compatibility agent, inorganic filler, antioxidant, lubricant, colouring agent etc..
Many physico-chemical properties (such as melt viscosity, melt index) of blend polymer are mainly by forming its polymer
Species and proportion of composing determine.Type of polymer essentially dictates the " compatibility between blend component
(compatibility) ", compatibility is one of the interphase interaction of different polymer and measured, and makees when between different polymer
It is referred to as (miscible) system of dissolving each other when stable and uniform on molecular scale mixes with it relatively by force, can be made；Other polymer
Between interaction it is slightly weak, although can not be dissolved each other in molecular scale, but still can disperse in nanoscale stable and uniform, claim it is this kind of
Blend is compatible (compatible) system；The interphase interaction of other polymer is very weak, even if being forced to mix, it
Also tend to form respective phase region, this kind of blend is then incompatible (incompatible) system.Blend polymer
Glass transition temperature (" Tg") information can as between each component compatibility quality simple basis for estimation【《Multicomponent gathers
Compound-principle, structure and performance》, kingdom, which builds, writes, and 2013, p.20-22】If blend keeps the glass of raw material components respectively
Glass transition temperature, then compatibility is bad between showing component, and when blend only has a glass transition temperature, then table
Compatibility is preferable between bright component.In the case where type of polymer determines, (such as melt glues some physicochemical properties of blend
Degree, melt index etc.) with its proportion of composing certain functional relation be present【《The plastic engineering handbook first volume》, Huang Rui chief editors,
2000, p.633-637；Melt Rheology of Polymer Blends from Melt Flow Index,
International Journal of Polymeric Materials,1984,10,p.213-235】, people can be accordingly
Substantially speculate even blend of the design with special properties.In the bad co-mixing system of some compatibilities, it may occur however that altogether
Mixed thing viscosity is less than the situation of raw material components【《JRG-Fourth statistics》, Jin Riguang work, 1998, p.630-633】, there is the phenomenon
The reason for there is no final conclusion at present, overall viscosity declines after the interface sliding that one of which is construed between different phases causes mixing.
Similar phenomenon has not been reported in the preferable blend system of compatibility, if more than being used in the preferable system of compatibility
Phenomenon, there must be great potentiality.
The theory property of some polyblends can be substantially speculated using addition rule, its addition theory can be used such as
Lower formula expression：
P=c1P1+c2P2
P be blend property, c1And P1For the concentration and property of component 1；c2And P2For the concentration and property of component 2.This
The thermoplastic cellulose of invention and the property (P) of aliphatic aromatic copolyester blends, such as apparent melt viscosity, melt index
Etc. the numerical value that theoretical prediction can be calculated using addition rule, that is, it is defined as " addition theoretical value ", the numerical value can be with experiment
The numerical value such as the apparent viscosity of detection, melt index compare.The concentration of component can use mass fraction or volume fraction to express, this
Invention selection calculates theoretical numerical value with mass fraction.
The blend of the concrete embodiment of the present invention includes cellulose acetate-butyrate and Biodegradable polyester such as fat
Fat race aromatic copolyester include poly terephthalic acid-co- tetramethylene adipates (PBAT), poly terephthalic acid-co- oneself two
Sour glycol ester (PEAT), poly terephthalic acid-co- EGS ethylene glycol succinates (PEST) and poly terephthalic acid-co- succinic acid
Butanediol ester (PBST) etc., composition include the cellulose acetate-butyrate of 20% to 80% quality and the fat of 80% to 20% quality
Fat race aromatic copolyester, it is characterised in that the melt viscosity of blend is in low shear rate (such as 100s-1) under the conditions of two kinds of ratio
The mixing addition theoretical value at least low 20% of initiation material.The melt viscosity of some blends more preferably formed is in low sheraing speed
Rate (such as 100s-1) under the conditions of it is at least lower by 30% than the mixing addition theoretical value of two kinds of initiation materials；Some most preferred groups into be total to
The melt viscosity of mixed thing is in low shear rate (such as 100s-1) under the conditions of it is at least lower than the mixing addition theoretical value of two kinds of initiation materials
35%.
The blend of the concrete embodiment of the present invention includes cellulose acetate-butyrate and Biodegradable polyester such as fat
Fat race aromatic copolyester include poly terephthalic acid-co- tetramethylene adipates (PBAT), poly terephthalic acid-co- oneself two
Sour glycol ester (PEAT), poly terephthalic acid-co- EGS ethylene glycol succinates (PEST) and poly terephthalic acid-co- succinic acid
Butanediol ester (PBST) etc., composition include the cellulose acetate-butyrate of 20% to 80% quality and the fat of 80% to 20% quality
Fat race aromatic copolyester, it is characterised in that the melt viscosity of blend is in high-rate of shear (such as 1000 or 1363s-1) under the conditions of
Mixing addition theoretical value than two kinds of initiation materials is at least low by 20%.The melt viscosity of some blends more preferably formed is in height
Shear rate (such as 1000 or 1363s-1) under the conditions of it is at least lower by 25% than the mixing addition theoretical value of two kinds of initiation materials；Some are most
The melt viscosity of the blend preferably constituted is in high-rate of shear (such as 1000 or 1363s-1) under the conditions of than two kinds of initiation materials
Mix addition theoretical value at least low 30%.
The blend of the concrete embodiment of the present invention includes cellulose acetate-butyrate and Biodegradable polyester such as fat
Fat race aromatic copolyester include poly terephthalic acid-co- tetramethylene adipates (PBAT), poly terephthalic acid-co- oneself two
Sour glycol ester (PEAT), poly terephthalic acid-co- EGS ethylene glycol succinates (PEST) and poly terephthalic acid-co- succinic acid
Butanediol ester (PBST) etc., composition include the cellulose acetate-butyrate of 20% to 80% quality and the fat of 80% to 20% quality
Fat race aromatic copolyester, it is characterised in that the melt index of blend than two kinds of initiation materials mixing addition theoretical value at least
It is high by about 10%.The melt index of some blends more preferably formed is at least higher than the mixing addition theoretical value of two kinds of initiation materials
40%；Some most preferred groups into blend melt index it is at least higher than the mixing addition theoretical value of two kinds of initiation materials
60%.
A kind of method for preparing thermoplastic cellulose and aliphatic aromatic copolyester blends of the present invention.This method exists
The aliphatic of the thermoplastic cellulose containing 20% to 80% quality and 80% to 20% quality fragrance in one continuous process
Race's copolyesters is uniformly mixed in the molten state, and extruding pelletization its prepare blend be characterised by that its melt viscosity exists
Low shear rate (100s-1) under the conditions of it is at least lower by 20% than the blending addition theoretical value of two kinds of initiation materials；In high-rate of shear
(1000 or 1363s-1) under the conditions of it is at least lower by 20% than the blending addition theoretical value of two kinds of initiation materials.
The blend " unusually " formed by a certain percentage of the present invention, " unexpectedly " have more fine than pure thermoplasticity
The lower apparent shear viscosity of the mixing addition theoretical value of dimension element and aliphatic aromatic copolyesters initiation material, i.e., " apparent
" matrix " curve is presented in viscosity-composition " graph of a relation, it is existing to show as " melt viscosity trap " (Melt Viscosity Well)
As showing that the blend has " anti-synergistic effect " (Antagonistic Effect or Anti- of apparent viscosity
Synergistic Effect)。
The blend " unusually " formed by a certain percentage of the present invention, " unexpectedly " have more fine than pure thermoplasticity
Higher melt index (the MFR of the mixing addition theoretical value of dimension element and aliphatic aromatic copolyesters initiation material：Melt Flow
Rate), i.e., in " melt index-composition " graph of a relation, " convex " curve is presented, shows as " melt index peak " (MFR
Peak) phenomenon, show that the blend has " cooperative effect " (the Synergistic Effect) of melt index.
The number-average molecular weight of the blend of the present invention at least above 20000g/mol, weight average molecular weight at least above
60000g/mol.The number-average molecular weight of the blend of the present invention is preferably at least more than 40000g/mol, and weight average molecular weight is preferably extremely
It is more than 80000g/mol less.
4. prepare the method for thermoplastic cellulose and biodegradable aliphatic aromatic copolyester blends
The continuous fusion preparation method of the present invention includes two-step method and one-step method.In two-step method, thermoplastic cellulose powder
End first passes around single screw rod or double screw extruder is granulated, then thermoplastic fibre crude granule and aliphatic aromatic copolyesters
After particle is well mixed according to a certain percentage, then blend of particles is added to a feeding machine according to certain feed rate
The spout of one double screw extruder.Feeding machine can be that weight-loss type feeding machine can also be volume type feeding machine.Another
Concrete embodiment is respectively thermoplastic fibre crude granule and aliphatic aromatic copolyester particles according to one using two feeding machines
Fixed feeding ratio is dosed on a double screw extruder and carries out extruding pelletization respectively.
The one-step method of the present invention is granulated thermoplastic fibres element powder without hot-working and directly pressed using a feeding machine
Certain feed rate is added into the spout of double screw extruder, while aliphatic aromatic copolyester particles are fed with another
Material machine is added into the spout of double screw extruder by certain feed rate, carries out twin-screw extrusion, and extrusion batten passes through water
Groove or underwater cutpellet, prepare blends particles.Extrudate can also pass through air-cooled and then pelletizing with anhydrous process.
The extrusion temperature for being suitable for the present invention is 140 DEG C to thermoplastic cellulose and the heat point of aliphatic aromatic copolyesters
Solve the low person of temperature.The extrusion temperature being generally adapted includes 140 DEG C to 240 DEG C.The rotating speed of extruder includes 50rpm to 1500rpm,
Preferably 100rpm to 800rpm.
There are many kinds to include kneading machine, Farrel continuous mixers, Banbury suitable for the melt blending equipment of the present invention
Mixer, single screw extrusion machine, double screw extruder, multi-screw extruder (more than two screw rod), reciprocating Single screw extrusion
Machine such as Buss reciprocating single-bolt extruder (Buss Ko-Kneader) etc..Preferable method is continuous fusion blending extrusion side
Method includes double screw extrusion method.Include the double screw extruder of different designs suitable for the crowded machine of continuous twin-screw of the present invention,
Such as ZSK Mcc18 equidirectional parallel double-screw extruders of German Coperion productions etc..
Thermoplastic cellulose prepared by the method for the twin-screw continuous fusion coextrusion that the present invention is shown and aliphatic fragrance
Race's polyester blending has the low melt viscosity of " unexpected ".A kind of embody of the present invention is under the same conditions, altogether
Mixing addition theoretical value of the melt viscosity of mixed thing less than thermoplastic cellulose and aliphatic aromatic copolyesters initiation material.Should
Viscosity, which reduces, has generality, is included in compared with low shear rate such as 100s-1With in higher shear rate such as 1000 or 1363s-1.In 100s-1Under shear rate, the melt viscosity of its blend is at least lower than the mixing addition theoretical value of two kinds of initiation materials
20%.Some more preferably form, and (mass ratio of copolyesters and thermoplastic cellulose is 65%:35% to 35%:65%) blending
The melt viscosity of thing is at least lower by 30% than the mixing addition theoretical value of two kinds of initiation materials, some most preferred groups into (copolyesters with
The mass ratio of thermoplastic cellulose is 35%:65%) mixing addition reason of the melt viscosity of blend than two kinds of initiation materials
By value at least low 35%.In 1000 or 1363s-1Under shear rate, the mixing of the melt viscosity of blend than two kinds of initiation materials
Addition theoretical value at least low 20%, some are more preferably formed, and (mass ratio of copolyesters and thermoplastic cellulose is 65%:35% to
20%:80%) melt viscosity of blend is at least lower by 25% than the mixing addition theoretical value of two kinds of initiation materials, and some are optimal
(mass ratio of copolyesters and thermoplastic cellulose is 35% to choosing composition:65% to 20%:80%) melt viscosity of blend
Mixing addition theoretical value than two kinds of initiation materials is at least low by 30%.
Thermoplastic fibres element and one kind of aliphatic aromatic copolyester blends material prepared by the present invention embodies
Mixing addition theoretical value of the melt index of blend higher than two kinds of initiation materials.The high melt index of the blend preferably constituted
In the mixing addition theoretical value at least about 10% of two kinds of initiation materials, (the matter of copolyesters and thermoplastic cellulose is more preferably formed
Amount is than being 65%:35% to 20%:80%) mixing addition theoretical value of the melt index of blend higher than two kinds of initiation materials
At least 40%, most preferred group is into (mass ratio of copolyesters and thermoplastic cellulose is 35%:65%) melting of blend refers to
Number body can be higher than the mixing addition theoretical value at least 60% of two kinds of initiation materials.
5. prepare the side of thermoplastic cellulose and biodegradable aliphatic aromatic copolyester blends fibre
Method
The present invention announces a kind of thermoplastic cellulose prepared with the special rheological equationm of state and aliphatic aromatic copolyesters
The method of blend thermoplastic fibre product, it is characterised in that the blend by 20% to 80% quality thermoplastic cellulose with
The aliphatic aromatic copolyesters composition of 80% to 20% quality.The continuous fusion extrusion blending method of the blend by mentioned earlier
It is prepared.The melt viscosity of blend is in low shear rate (100s-1) under the conditions of it is at least lower by 20% than addition theoretical value；In height
Shear rate (1000 or 1363s-1) under the conditions of it is at least lower by 20% than addition theoretical value.Blend has more preferable than initiation material
Spinning workability energy, blend is squeezed on a screw extruder after plastifying, melting and measure by spinneret orifice in this method
Go out to form melt stream, through cooling down, stretching prepare fiber.
The blend of the present invention passes through a single screw extrusion machine or a double screw extruder during melt spinning
Plasticizing, fusing extrusion.Extruder barrel temperature is 160 DEG C to 240 DEG C, and the temperature being more suitable for is 180 DEG C to 220 DEG C.Melt meter
It can be a gear pump to measure device.Cooling includes the cooling gas parallel with machine direction, also includes vertical with machine direction
Cooling gas, cooling gas can be air, nitrogen, inert gas or other gases.
The method of the present invention such as also oils, wound at the step including fiber.Fiber may also pass through multistage stretching process, multistage
Stretching can be realized by a series of rollers that are heating or not heating, be higher than what is previously passed through by the rotating speed of roller after fiber
Roller.The fiber of preparation can be filament fiber, for textile industry.The fiber of preparation can also be cut into short fibre, for preparing
The bonded fabric products such as fabric hot rolled nonwoven fabrics (Bonded Carded Web, BCW), spunlace non-woven cloth (Spunlace).
Fiber in the present invention can be one-component fiber or multicomponent fibre.Multicomponent fibre is by 2 or two
Extruder system more than individual, the standby melt of each extrusion mechanism pass through a multicomponent with the standby melt of other extrusion mechanisms
Spinneret is prepared into multicomponent fibre.The configuration of multicomponent fibre can be core-skin type, island shape, side-by-side type etc..
The thermoplastic cellulose and aliphatic aromatic that the continuous extrusion blend method announced using the present invention is prepared
There are than two kinds pure raw materials to mix the lower melt viscosity of addition theoretical value for polyester blending fibres, blend, and higher is molten
Melt index, the fine fibre of not inter-adhesive function admirable can be obtained, achieve preferable technique effect.
Brief description of the drawings
At 180 DEG C of Fig. 1, the relation of each PBAT/CAB particles apparent shear viscosity and shear rate.
At 180 DEG C of Fig. 2, each PBAT/CAB particles are in 100s-1Shear rate under, between apparent shear viscosity and composition
Relation, dotted line is addition theoretical calculation numerical value line in figure.
At 180 DEG C of Fig. 3, each PBAT/CAB particles are in 1363s-1Shear rate under, between apparent shear viscosity and composition
Relation, dotted line is addition theoretical calculation numerical value line in figure.
The DSC temperature lowering curves of each PBAT/CAB particles of Fig. 4.
Second of heating curve of DSC of each PBAT/CAB particles of Fig. 5.
Each PBAT/CAB particles glass transition temperatures of Fig. 6 and the relation of composition.
The TGA curves of each PBAT/CAB particles of Fig. 7 in air atmosphere.
Relation between the melt index (190 DEG C, 2.16kg) of each PBAT/CAB particles of Fig. 8 and composition, dotted line is in figure
Addition theoretical calculation numerical value line.
At 180 DEG C of Fig. 9, the relation of each PBST/CAB particles apparent shear viscosity and shear rate.
At 180 DEG C of Figure 10, each PBST/CAB particles are in 100s-1Shear rate under, between apparent shear viscosity and composition
Relation, dotted line is addition theoretical calculation numerical value line in figure.
At 180 DEG C of Figure 11, each PBST/CAB particles are in 1000s-1Shear rate under, apparent shear viscosity and composition
Between relation, dotted line is addition theoretical calculation numerical value line in figure.
Relation between the melt index (190 DEG C, 2.16kg) of each PBST/CAB particles of Figure 12 and composition, dotted line in figure
For addition theoretical calculation numerical value line.
At 180 DEG C of Figure 13, the relation of each PBAT/CAP particles apparent shear viscosity and shear rate.
At 180 DEG C of Figure 14, each PBAT/CAP particles are in 100s-1Shear rate under, between apparent shear viscosity and composition
Relation, dotted line is addition theoretical calculation numerical value line in figure.
At 180 DEG C of Figure 15, each PBAT/CAP particles are in 1000s-1Shear rate under, apparent shear viscosity and composition
Between relation, dotted line is addition theoretical calculation numerical value line in figure.
Relation between the melt index (190 DEG C, 2.16kg) of each PBAT/CAP particles of Figure 16 and composition, dotted line in figure
For addition theoretical calculation numerical value line.
The DSC temperature lowering curves of each PBAT/CAP particles of Figure 17.
Second of heating curve of DSC of each PBAT/CAP particles of Figure 18.
The drafting force of each PBAT/CAB samples of Figure 19 and the relation of drafting rate.
Ratio (the V of drafting rate and piston speed during each PBAT/CAB sample fractures of Figure 20haul-off,break/Vpiston) with
The relation of composition.
The present invention carries out performance measurement by the following method：
Melt index (MFR) assay method：By the standards of ISO 1133, using Lloyd DAVENPORTTM MFI-10/230
Fusion index instrument determines, 190 DEG C, weight loading 2.16kg, port mould diameter 2.095mm of barrel temperature, length 8mm, during preheating
Between be 4min, cut sample automatically every setting time, take 5 times and average, represent to survey with the grams of every 10 minutes (g/10min)
Determine result.
Rheological behaviour assay method：Using Malvern Instruments Rosand RH7 thermal high capillary rheometers
Measure, processing software is Launch8.60 version.Test is from the sensor and 16/ that pressure is 10000Psi
1.0/180 circular hole capillary die.It is compacted when filling sample for filling in batches, the precompressed by 0.5MPa twice is needed before test
With the warm of 2 minutes, with ensure particle at a temperature selected (180 DEG C) completely melting and compacting.
Thermogravimetric analysis (TGA)：Test is enterprising in the Discovery series thermogravimetric analyzers of TA Instruments companies
OK, it is TA Instruments Trios 3.1.4 versions to handle software.The temperature stabilization for needing to wait balance cavity before test is 40
℃.During test, weigh 5~10mg samples and be placed in ceramic crucible, tested in the air atmosphere that flow velocity is 20mL/min,
Temperature elevating range is 30~600 DEG C, and heating rate is 10 DEG C/min.
Thermal performance analysis (DSC)：Test the Discovery series of differential scanning amounts in the production of TA Instruments companies
Carried out on hot instrument (DSC), processing software is TA Instruments Trios 3.1.5 versions, and the DSC instrument is furnished with
The mechanical refrigeration annexes of Refrigerated Cooling System 90.Measurement atmosphere is 50mL/min nitrogen, needed for test
Sample size is 5~10mg.Test program is as follows：First by temperature stabilization at 40 DEG C, then 250 DEG C and constant temperature are warming up to 10 DEG C/min
2min removes thermal history, cools to -70 DEG C with 10 DEG C/min afterwards, is then warming up to 250 DEG C with 10 DEG C.Record temperature-fall period with
And second of temperature-rise period, with the hot property of study sample.Tested by DSC, there can be the crystallization that software immediately arrives at sample
Temperature (" Tc"), melting temperature (" Tm"), glass transition (" Tg"), the information such as heat content change (" △ H ").
Embodiment
The present invention is specifically described by the following examples.Herein it is important to point out that once embodiment is only right
It is further described in the present invention, it is impossible to be interpreted as limiting the scope of the invention, the those of skill in the art in the field
Some nonessential modifications and adaptations can be made according to foregoing invention content.
【Comparative example 1】
Used poly terephthalic acid-co- tetramethylene adipates (PBAT) are by BASF Aktiengesellschaft in the present invention
Production, the trade mark areF BX 7011.Raw materialThe PBAT particles of F BX 7011, with U.S. Thermo
The PolyLab HAAKE of Fisher scientific ＆ technical corporationTMRheomex OS PTW16 parallel dual-screw extruding machines (screw diameter 16mm,
L/D=40) extruding pelletization, as a comparison case.The extruder is totally 11 sections, numbering 1-11 from spout to mouth mold, wherein the 1st section
The effect of charging is only served, can not be heated.The subsidiary volume type particle feeder of extruder, being used for after demarcation willThe PBAT raw materials of F BX 7011 are fed in twin-screw, blanking velocity 2100g/hr.The temperature of extruder 2-11 sections
Respectively：140 DEG C, 150 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C and 160 DEG C, screw speed
200rpm is set in, moment of torsion is in 50-60%.The extruder is furnished with a diameter of 3mm circular mouth mold, and batten passes through from die extrusion
After water-bath cooling, 3mm or so cylindrical particle is cut into pelleter.Particle is collected, 4hr is taken out in 60 DEG C of vacuum drying chambers
Afterwards, encapsulate standby.Melt index of the particle under 190 DEG C, 2.16kg is 18.98g/10min.
【Comparative example 2】
Used cellulose acetate-butyrate (CAB) produces from Eastman companies of the U.S. in this comparative example, and the trade mark is
EastmanTMCAB-531-1.Raw material EastmanTMCAB-531-1 powder, with Thermo Fisher scientific ＆ technical corporation of the U.S.
PolyLab HAAKETMRheomex OS PTW16 parallel dual-screw extruding machines (screw diameter 16mm, L/D=40) extrusion is made
Grain, as a comparison case.The extruder is totally 11 sections, numbering 1-11 from spout to mouth mold, wherein the 1st section of work for only serving charging
With can not heat.The subsidiary volume type powder feeder of extruder, it is used for after demarcation by EastmanTM CAB-531-1
Raw material is fed in twin-screw, blanking velocity 1000g/hr.The temperature of extruder 2-11 sections is respectively：140℃,150℃,160
DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C and 160 DEG C, screw speed is set in 200rpm, and moment of torsion is in 60-
70%.The extruder be furnished with a diameter of 3mm circular mouth mold, batten from die extrusion after water-bath cooling, with pelletizing machine-cut
Into 3mm or so cylindrical particle.Particle is collected, after taking out 4hr in 60 DEG C of vacuum drying chambers, encapsulation is standby.The particle is 190
DEG C, the melt index under 2.16kg is 8.96g/10min.
【Embodiment 1】
The PBAT of F BX 7011 and EastmanTMCAB-531-1 is in PolyLab HAAKE mentioned aboveTM
Melt blending extruding pelletization in Rheomex OS PTW16 parallel dual-screw extruding machines.At the 1st section of extruder, calibrated body
Product formula particle feeder is used forThe feeding of the PBAT particles of F BX 7011, speed are：1680g/hr, demarcate simultaneously
Volume type powder feeder afterwards is used for EastmanTMThe feeding of CAB-531-1 powder, speed are：420g/hr.Extruder
The temperature of 2-11 sections is respectively：140 DEG C, 150 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C and 160
DEG C, screw speed is set in 200rpm, and moment of torsion is in 50-60%.The extruder be furnished with a diameter of 3mm circular mouth mold, batten from
Die extrusion is cut into 3mm or so cylindrical particle with pelleter after water-bath cooling.Particle is collected, is done in 60 DEG C of vacuum
After taking out 4hr in dry case, encapsulation is standby.Melt index of the particle under 190 DEG C, 2.16kg is 18.52g/10min.
【Embodiment 2】
The PBAT of F BX 7011 and EastmanTMCAB-531-1 is in PolyLab HAAKE mentioned aboveTM
Melt blending extruding pelletization in Rheomex OS PTW16 parallel dual-screw extruding machines.At the 1st section of extruder, calibrated body
Product formula particle feeder is used forThe feeding of the PBAT particles of F BX 7011, speed are：1365g/hr, demarcate simultaneously
Volume type powder feeder afterwards is used for EastmanTMThe feeding of CAB-531-1 powder, speed are：735g/hr.Extruder
The temperature of 2-11 sections is respectively：140 DEG C, 150 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C and 160
DEG C, screw speed is set in 200rpm, and moment of torsion is in 45-55%.The extruder be furnished with a diameter of 3mm circular mouth mold, batten from
Die extrusion is cut into 3mm or so cylindrical particle with pelleter after water-bath cooling.Particle is collected, is done in 60 DEG C of vacuum
After taking out 4hr in dry case, encapsulation is standby.Melt index of the particle under 190 DEG C, 2.16kg is 21.23g/10min.
【Embodiment 3】
The PBAT of F BX 7011 and EastmanTMCAB-531-1 is in PolyLab HAAKE mentioned aboveTM
Melt blending extruding pelletization in Rheomex OS PTW16 parallel dual-screw extruding machines.At the 1st section of extruder, calibrated body
Product formula particle feeder is used forThe feeding of the PBAT particles of F BX 7011, speed are：1050g/hr, demarcate simultaneously
Volume type powder feeder afterwards is used for EastmanTMThe feeding of CAB-531-1 powder, speed are：1050g/hr.Extruder
The temperature of 2-11 sections is respectively：140 DEG C, 150 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C and 160
DEG C, screw speed is set in 200rpm, and moment of torsion is in 45-55%.The extruder be furnished with a diameter of 3mm circular mouth mold, batten from
Die extrusion is cut into 3mm or so cylindrical particle with pelleter after water-bath cooling.Particle is collected, is done in 60 DEG C of vacuum
After taking out 4hr in dry case, encapsulation is standby.Melt index of the particle under 190 DEG C, 2.16kg is 20.81g/10min.
【Embodiment 4】
The PBAT of F BX 7011 and EastmanTMCAB-531-1 is in PolyLab HAAKE mentioned aboveTM
Melt blending extruding pelletization in Rheomex OS PTW16 parallel dual-screw extruding machines.At the 1st section of extruder, calibrated body
Product formula particle feeder is used forThe feeding of the PBAT particles of F BX 7011, speed are：735g/hr, demarcate simultaneously
Volume type powder feeder afterwards is used for EastmanTMThe feeding of CAB-531-1 powder, speed are：1365g/hr.Extruder
The temperature of 2-11 sections is respectively：140 DEG C, 150 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C and 160
DEG C, screw speed is set in 200rpm, and moment of torsion is in 45-55%.The extruder be furnished with a diameter of 3mm circular mouth mold, batten from
Die extrusion is cut into 3mm or so cylindrical particle with pelleter after water-bath cooling.Particle is collected, is done in 60 DEG C of vacuum
After taking out 4hr in dry case, encapsulation is standby.Melt index of the particle under 190 DEG C, 2.16kg is 19.83g/10min.
【Embodiment 5】
The PBAT of F BX 7011 and EastmanTMCAB-531-1 is in PolyLab HAAKE mentioned aboveTM
Melt blending extruding pelletization in Rheomex OS PTW16 parallel dual-screw extruding machines.At the 1st section of extruder, calibrated body
Product formula particle feeder is used forThe feeding of the PBAT particles of F BX 7011, speed are：420g/hr, demarcate simultaneously
Volume type powder feeder afterwards is used for EastmanTMThe feeding of CAB-531-1 powder, speed are：1680g/hr.Extruder
The temperature of 2-11 sections is respectively：140 DEG C, 150 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C, 160 DEG C and 160
DEG C, screw speed is set in 200rpm, and moment of torsion is in 55-65%.The extruder be furnished with a diameter of 3mm circular mouth mold, batten from
Die extrusion is cut into 3mm or so cylindrical particle with pelleter after water-bath cooling.Particle is collected, is done in 60 DEG C of vacuum
After taking out 4hr in dry case, encapsulation is standby.Melt index of the particle under 190 DEG C, 2.16kg is 15.86g/10min.
【Embodiment 6】
7 kinds of particles of all of the above, including comparative example 1-2 and embodiment 1-5, in Malvern Instruments
Rheological behaviour measure is carried out on Rosand RH7 thermal high capillary rheometers, method of testing is selected as described above, during test
Select the apparent shear viscosity determined under following shear rate：100,192,369,709,1363,2615 and 5019s-1..At 180 DEG C
Under the apparent shear viscosity of each particle and the relation of shear rate see Fig. 1.Its medium shear rate is in 100s-1And 1363s-1Under
The relation of apparent shear viscosity and composition is shown in Fig. 2 and Fig. 3 respectively, and concrete numerical value is listed in Tables 1 and 2.
Obvious shear shinning phenomenon as can see from Figure 1, i.e. the bigger shear viscosity of shear rate is smaller, this phenomenon
It is very common in polymeric system, show that the fundamental property of system after being blended does not have significant change.And in most of situation
Especially under high-rate of shear, the apparent shear viscosity of mixture is mostly under the same conditions below two kinds of pure raw materials, i.e., two kinds
Viscosity declines after raw material mixing.Fig. 2 and Fig. 3 specifically are seen, can find the apparent shear viscosity of particle after being blended nearly all than appointing
What pure initiation material is all small, and viscograph is into " matrix " i.e. unexpected " viscosity trap " phenomenon, the grain after this explanation blending
Son no matter at a high speed or low velocity shear under viscosity diminish, this property seldom occurs in compatible polyblend.
Some performance parameters after polymer blending can be speculated with addition theoretical value, specifically true according to below equation
It is fixed：
P=c1P1+c2P2
P is addition theoretical values in formula, P1For the corresponding parametric values of component in mixture 1, c1For its mass fraction, P2For
The corresponding parametric values of component 2, c in mixture2For its mass fraction.If the measured value of mixture parameter and the addition theoretical value phase
Difference is bigger, and collaboration (or anti-collaboration) effect is more notable between showing component.
As can be found from Table 1, when shear rate is 100s-1When, actual blend apparent shear viscosity is than addition theoretical value
Low about 20.3% (embodiment 1) is to 34.4% (embodiment 4).
As can be found from Table 2, when shear rate is 1363s-1When, actual blend apparent shear viscosity is than addition theoretical value
Low about 20.7% (embodiment 1) is to 31.9% (embodiment 4).
【Embodiment 7】
7 kinds of particles of all of the above, including comparative example 1-2 and embodiment 1-5, as described above the step of carried out difference
Show scanning calorimetric (DSC) test, temperature lowering curve and second of heating curve are shown in Fig. 4 and Fig. 5 respectively.Can be with software directly therefrom
Obtain crystallization temperature (" Tc"), melting temperature (" Tm"), glass transition (" Tg"), the information such as heat content change (" △ H "), specifically
Numerical value is listed in table 3.Each particle glass transition temperature (" Tg") with composition relation see Fig. 6.
It can be seen that its crystallinity is gradually reduced when PBAT contents reduce in blend from Fig. 4 and Fig. 5, knot is shown
Brilliant temperature is gradually reduced and peak crystallization diminishes, when PBAT mass fractions be down to 50% and it is following when, do not observe obvious
Crystallization and melting peak (detailed data is shown in Table, 3).All particles only have a glass transition temperature (" Tg"), show to be blended
The compatibility respectively formed in particle is fine, and TgNumerical value raised with the increase of CAB contents, see Fig. 6.
【Embodiment 8】
7 kinds of particles of all of the above, including comparative example 1-2 and embodiment 1-5, as described above the step of carried out heat
Weight analysis (TGA) are tested, and test result is shown in Fig. 7.From the figure, it can be seen that the heat decomposition curve of particle is substantially all two after blending
Between individual comparative example curve, show that the pyrolytic that front and rear CAB and PBAT is blended does not have too big change, this is consistent with expection
Close.
【Embodiment 9】
7 kinds of particles of all of the above, including comparative example 1-2 and embodiment 1-5, as described above the step of melted
Melt index (MFR) test (190 DEG C, 2.16kg), the relation between the MFR numerical value and composition that measure is shown in Fig. 8.Obtained from Fig. 8
Concrete numerical value is listed in table 4, including " addition theoretical value " mentioned above.
As can be found from Table 4, for PBAT and CAB after melt blending, the actual melt index of embodiment 1 is more theoretical than addition
It is worth high 1.54g/10min, percentage is about 9.1%；The actual melt index of embodiment 4 is higher 7.36g/ than addition theoretical value
10min, percentage are about 59.1%, are that percent value is maximum in embodiment.The high melt index of all these exceptions is all
It is unexpected, it is rare in the good polymer blends of compatibility, and not yet sent out in CAB and PBAT blends
Existing phenomenon.
【Comparative example 3】
Used poly terephthalic acid-co- succinic acid-butanediol esters (PBST) are self-control in the present invention, and preparation process is joined
According to【Zhu Pengfei, the nucleator of poly terephthalic acid -co- succinic acid-butanediol ester (PBST) and modification by copolymerization research, 2013, it is large
Scholar's paper】, succinic acid and terephthalic acid (TPA) respectively account for the 50% of total diacid inventory mol ratio, and butanediol is slightly excessive to feed intake, and is made
PBST intrinsic viscosities about 1.20, wherein being not added with nucleator and other auxiliary agents.PBST particles are made by oneself, with U.S. Thermo
The PolyLab HAAKE of Fisher scientific ＆ technical corporationTMRheomex OS PTW16 parallel dual-screw extruding machines (screw diameter 16mm,
L/D=40) extruding pelletization, as a comparison case.The extruder is totally 11 sections, numbering 1-11 from spout to mouth mold, wherein the 1st section
The effect of charging is only served, can not be heated.The subsidiary volume type particle feeder of extruder, being used for after demarcation will self-control
PBST particles are fed in twin-screw, blanking velocity 1800g/hr.The temperature of extruder 2-11 sections is respectively：160℃,170℃,
180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C and 180 DEG C, screw speed is set in 200rpm, and moment of torsion exists
55-61.5%.The extruder is furnished with a diameter of 3mm circular mouth mold, and batten after water-bath cooling, uses pelletizing from die extrusion
Cylindrical particle of the machine-cut into 3mm or so.Particle is collected, after taking out 4hr in 60 DEG C of vacuum drying chambers, encapsulation is standby.The particle
Melt index under 190 DEG C, 2.16kg is 5.73g/10min.
【Comparative example 4】
Used cellulose acetate-butyrate (CAB) produces from Eastman companies of the U.S. in this comparative example, and the trade mark is
EastmanTMCAB-381-0.5.Raw material EastmanTMCAB-381-0.5 powder, it is public with U.S. Thermo Fisher science and technology
The PolyLab HAAKE of departmentTMRheomex OS PTW16 parallel dual-screw extruding machines (screw diameter 16mm, L/D=40) are extruded
It is granulated, as a comparison case.The extruder is totally 11 sections, numbering 1-11 from spout to mouth mold, wherein the 1st section only serves charging
Effect, can not be heated.The subsidiary volume type powder feeder of extruder, it is used for after demarcation by EastmanTM CAB-
381-0.5 raw materials are fed in twin-screw, blanking velocity 900g/hr.The temperature of extruder 2-11 sections is respectively：160℃,170
DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C and 180 DEG C, screw speed is set in 200rpm, moment of torsion
In 68-70%.The extruder is furnished with a diameter of 3mm circular mouth mold, and batten after water-bath cooling, uses pelletizing from die extrusion
Cylindrical particle of the machine-cut into 3mm or so.Particle is collected, after taking out 4hr in 60 DEG C of vacuum drying chambers, encapsulation is standby.The particle
Melt index under 190 DEG C, 2.16kg is 6.01g/10min.
【Embodiment 10】
Make PBST particles and Eastman by oneselfTMCAB-381-0.5 is in PolyLab HAAKE mentioned aboveTM Rheomex
Melt blending extruding pelletization in OS PTW16 parallel dual-screw extruding machines.At the 1st section of extruder, calibrated volume type particle
Feeder is used for the feeding for making PBST particles by oneself, and speed is：1440g/hr, while calibrated volume type powder feeder quilt
For EastmanTMThe feeding of CAB-381-0.5 powder, speed are：360g/hr.The temperature of extruder 2-11 sections is respectively：
160 DEG C, 170 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C and 180 DEG C, screw speed is set in
200rpm, moment of torsion is in 53-57%.The extruder is furnished with a diameter of 3mm circular mouth mold, and batten is cold by water-bath from die extrusion
But after, 3mm or so cylindrical particle is cut into pelleter.Particle is collected, after taking out 4hr in 60 DEG C of vacuum drying chambers, encapsulation
It is standby.Melt index of the particle under 190 DEG C, 2.16kg is 8.15g/10min.
【Embodiment 11】
Make PBST particles and Eastman by oneselfTMCAB-381-0.5 is in PolyLab HAAKE mentioned aboveTM Rheomex
Melt blending extruding pelletization in OS PTW16 parallel dual-screw extruding machines.At the 1st section of extruder, calibrated volume type particle
Feeder is used for the feeding for making PBST particles by oneself, and speed is：1170g/hr, while calibrated volume type powder feeder quilt
For EastmanTMThe feeding of CAB-381-0.5 powder, speed are：630g/hr.The temperature of extruder 2-11 sections is respectively：
160 DEG C, 170 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C and 180 DEG C, screw speed is set in
200rpm, moment of torsion is in 52-54%.The extruder is furnished with a diameter of 3mm circular mouth mold, and batten is cold by water-bath from die extrusion
But after, 3mm or so cylindrical particle is cut into pelleter.Particle is collected, after taking out 4hr in 60 DEG C of vacuum drying chambers, encapsulation
It is standby.Melt index of the particle under 190 DEG C, 2.16kg is 11.89g/10min.
【Embodiment 12】
Make PBST particles and Eastman by oneselfTMCAB-381-0.5 is in PolyLab HAAKE mentioned aboveTM Rheomex
Melt blending extruding pelletization in OS PTW16 parallel dual-screw extruding machines.At the 1st section of extruder, calibrated volume type particle
Feeder is used for the feeding for making PBST particles by oneself, and speed is：900g/hr, while calibrated volume type powder feeder quilt
For EastmanTMThe feeding of CAB-381-0.5 powder, speed are：900g/hr.The temperature of extruder 2-11 sections is respectively：
160 DEG C, 170 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C and 180 DEG C, screw speed is set in
200rpm, moment of torsion is in 54.5-60%.The extruder is furnished with a diameter of 3mm circular mouth mold, and batten passes through water-bath from die extrusion
After cooling, 3mm or so cylindrical particle is cut into pelleter.Particle is collected, after taking out 4hr in 60 DEG C of vacuum drying chambers, envelope
Equipment is used.Melt index of the particle under 190 DEG C, 2.16kg is 13.02g/10min.
【Embodiment 13】
Make PBST particles and Eastman by oneselfTMCAB-381-0.5 is in PolyLab HAAKE mentioned aboveTM Rheomex
Melt blending extruding pelletization in OS PTW16 parallel dual-screw extruding machines.At the 1st section of extruder, calibrated volume type particle
Feeder is used for the feeding for making PBST particles by oneself, and speed is：630g/hr, while calibrated volume type powder feeder quilt
For EastmanTMThe feeding of CAB-381-0.5 powder, speed are：1170g/hr.The temperature of extruder 2-11 sections is respectively：
160 DEG C, 170 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C and 180 DEG C, screw speed is set in
200rpm, moment of torsion is in 62-68%.The extruder is furnished with a diameter of 3mm circular mouth mold, and batten is cold by water-bath from die extrusion
But after, 3mm or so cylindrical particle is cut into pelleter.Particle is collected, after taking out 4hr in 60 DEG C of vacuum drying chambers, encapsulation
It is standby.Melt index of the particle under 190 DEG C, 2.16kg is 13.69g/10min.
【Embodiment 14】
Make PBST particles and Eastman by oneselfTMCAB-381-0.5 is in PolyLab HAAKE mentioned aboveTM Rheomex
Melt blending extruding pelletization in OS PTW16 parallel dual-screw extruding machines.At the 1st section of extruder, calibrated volume type particle
Feeder is used for the feeding for making PBST particles by oneself, and speed is：300g/hr, while calibrated volume type powder feeder quilt
For EastmanTMThe feeding of CAB-381-0.5 powder, speed are：1200g/hr.The temperature of extruder 2-11 sections is respectively：
160 DEG C, 170 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C and 180 DEG C, screw speed is set in
200rpm, moment of torsion is in 61.5-70%.The extruder is furnished with a diameter of 3mm circular mouth mold, and batten passes through water-bath from die extrusion
After cooling, 3mm or so cylindrical particle is cut into pelleter.Particle is collected, after taking out 4hr in 60 DEG C of vacuum drying chambers, envelope
Equipment is used.Melt index of the particle under 190 DEG C, 2.16kg is 13.45g/10min.
【Embodiment 15】
7 kinds of particles of the above, including comparative example 3-4 and embodiment 10-14, in Malvern Instruments Rosand
Carry out rheological behaviour measure on RH7 thermal high capillary rheometers, method of testing as described above, during test selection measure with
Apparent shear viscosity under down cut speed：30,100,200,500,1000,2000 and 5000s-1.Each particle at 180 DEG C
The relation of apparent shear viscosity and shear rate is shown in Fig. 9.Its medium shear rate is in 100s-1And 1000s-1Under apparent shearing glue
The relation of degree and composition is shown in Figure 10 and Figure 11 respectively, and concrete numerical value is listed in table 5 and table 6.
Obvious shear shinning phenomenon as can see from Figure 9, i.e. the bigger shear viscosity of shear rate is smaller, this phenomenon
It is very common in polymeric system, show that the fundamental property of system after being blended does not have significant change.And in most of situation
Especially under high-rate of shear, the apparent shear viscosity of mixture is mostly under the same conditions below two kinds of pure raw materials, i.e., two kinds
Viscosity declines after raw material mixing.Figure 10 and Figure 11 specifically are seen, can find that the apparent shear viscosity of particle after being blended nearly all compares
Any pure initiation material is all small, and into " matrix " i.e. unexpected " viscosity trap " phenomenon, this illustrates after being blended viscograph
Particle no matter at a high speed or low velocity shear under viscosity diminish, this property is seldom sent out in compatible polyblend
It is raw.
Some performance parameters after polymer blending can be speculated with addition theoretical value, specifically true according to below equation
It is fixed：
P=c1P1+c2P2
P is addition theoretical values in formula, P1For the corresponding parametric values of component in mixture 1, c1For its mass fraction, P2For
The corresponding parametric values of component 2, c in mixture2For its mass fraction.If the measured value of mixture parameter and the addition theoretical value phase
Difference is bigger, and collaboration (or anti-collaboration) effect is more notable between showing component.
As can be found from Table 5, when shear rate is 100s-1When, actual blend apparent shear viscosity is than addition theoretical value
Low about 19.1% (embodiment 10) is to 62.9% (embodiment 13).
As can be found from Table 6, when shear rate is 1000s-1When, actual blend apparent shear viscosity is than addition theoretical value
Low about 35.0% (embodiment 10) is to 65.0% (embodiment 14).
【Embodiment 16】
7 kinds of particles of the above, including comparative example 3-4 and embodiment 10-14, as described above the step of melted
Index (MFR) tests (190 DEG C, 2.16kg), and the relation between the MFR numerical value and composition that measure is shown in Figure 15.Obtained from Figure 12
Concrete numerical value is listed in table 7, including " addition theoretical value " mentioned above.
As can be found from Table 7, PBST and CAB after melt blending, than addition manage by the actual melt index of embodiment 10
By high 2.36g/10min is worth, percentage is about 40.9%；The actual melt index of embodiment 13 is higher 7.78g/ than addition theoretical value
10min, percentage are about 131.6%, are that percent value is maximum in embodiment.The high melt index of all these exceptions is all
It is unexpected, it is rare in the good polymer blends of compatibility, and not yet sent out in PBST and CAB blends
Existing phenomenon.
【Comparative example 5】
In order to verify special low-shear viscosity in embodiment 1-5 and embodiment 10-14 and high fusion index phenomenon simultaneously
It is not universal phenomenon when biodegradable fatty race aromatic copolyester is blended with thermoplastic cellulose ester,F BX
7011 PBAT and another thermoplastic cellulose CAP (EastmanTMCAP 375E4000012) by with similar processing method
Carry out melt blending extrusion.The ratio of mixing elects PBAT/CAP (mass ratio) as：0/100,20/80,50/50,80/20 and 100/
0.Mixed process is equally in PolyLab HAAKETMCarried out in Rheomex OS PTW16 parallel dual-screw extruding machines, with extrusion
The volume type feeder that machine carries adds into the 1st section of extruder simultaneously in proportionThe PBAT of F BX 7011 and
EastmanTMCAP 375E4000012.The temperature of extruder 2-11 sections is respectively：160℃,170℃,180℃,180℃,180
DEG C, 180 DEG C, 180 DEG C, 180 DEG C, 180 DEG C and 180 DEG C, screw speed is set in 200rpm.The extruder is furnished with a diameter of 3mm
Circular mouth mold, after water-bath cooling, 3mm or so cylindrical particle is cut into pelleter from die extrusion batten.Collect
Particle, after 4 hours are taken out in 60 DEG C of vacuum drying chambers, encapsulation is standby.
The dried PBAT/CAP particles of five kinds of the above, method as described above determine capillary stream at 180 DEG C
Change nature, during test selection determine the apparent shear viscosity under following shear rate：30,100,200,500,1000,2000 Hes
5000s-1., test result is shown in Figure 13, from figure it can be found that the viscograph of most of stuff and other stuff two kinds of pure raw materials it
Between.Low shear rate (100s-1) and high-rate of shear (1000s-1) under apparent viscosity with composition relation be listed in Figure 14 respectively
And Figure 15, from figures 14 and 15 it can be seen that no matter in low shear rate (100s-1) or high-rate of shear (1000s-1)
Under, the shear viscosity of stuff and other stuff is near addition theoretical value, " melt that can not be as shown in Fig. 2, Fig. 3, Figure 10 and Figure 11
Viscosity trap " phenomenon.This shows " melt viscosity trap " phenomenon in Fig. 2, Fig. 3, Figure 10 and Figure 11, is the skill of " unexpected " really
Art effect.
The dried PBAT/CAP particles of five kinds of the above, method measure melt index (MFR) as described above, test
As a result Figure 16 is seen.From figure it can be found that in PBAT/CAP systems, " the melt index that is not presented just like Fig. 8 and Figure 12
Peak " phenomenon, opposite PBAT have also appeared a certain degree of melt index and decline after being mixed with CAP.This shows in Fig. 8 and Figure 12
" melt index peak " phenomenon, it is the technique effect of " unexpected " really.
Five kinds of PBAT/CAP particles of the above, method as described above have carried out DSC tests, temperature lowering curve and second
Heating curve is shown in Figure 17 and Figure 18 respectively.From Figure 17 and Figure 18 it can clearly be seen that after two kinds of raw material mixing of PBAT and CAP
Respective crystallization temperature is remained in that, respectively about 82 DEG C and 77 DEG C, and keep respective melting temperature, respectively about 134 DEG C
With 92 DEG C, although can't see CAP has obvious glass transition temperature (Tg), but the T that PBAT mixing is front and reargRemain at about-
29 DEG C, data above shows that PBAT in the blend and CAP compatibility are bad, and both, which exist, is separated, crystallization process point
Do not carried out in respective phase region.And it was found from Fig. 4 to Fig. 6, an only T after PBAT and CAB blendingsg, and crystallization process
There occurs significant change, i.e. PBAT and CAB compatibilities are good.
By above difference, present inventors have surprisingly found that, different celluloses and poly- aliphatic fragrance of the present invention
The blend performance difference that race's copolyesters is formed is very big, although such as CAP and CAB is thermoplastic fibre commonly used in the art
Element, but it differs huge with the blend composite properties of aliphatic aromatic copolyesters, the thermoplasticity having been surprisingly found that
Cellulose and aliphatic aromatic copolyester blends, what is especially but do not limited is " PBAT and CAB " and " PBST and CAB " blendings
Thing, there is good synergistic function, not only rheological property is good, and compatibility is also good, can widen starting significantly
The use range of raw material, while the energy consumption in material processing can be reduced..
【Embodiment 17】
7 kinds of PBAT/CAB particles of the above, including comparative example 1-2 and embodiment 1-5, the Malvern instrument company in the U.S.
The test of melt strength is carried out in Rosand RH7 capillary rheometers, and collects silk material.The capillary rheometer is equipped with
10000psi pressure sensor, a whole set of drawing-off deflector roll, and a diameter of 2.095mm cylinder " Haul-Off/
Melt Strength " special moulds.Expect that chamber temperature is set to 180 DEG C in experimentation.Before test starts, first divide 3-5 times to material chamber
Load about 50g samples altogether, be compacted every time with depression bar, after the completion of filling sample, then carry out the process of a precompressed and preheating, precompressed
Pressure is set as 0.5MPa, preheating time is 2 minutes.Then formally start to test, typical experimentation is as follows：Piston pushes
Speed is fixed on 5mm/min, and the tension force of silk material and diameter are controlled by adjusting drafting rate, drafting rate 5 minutes it
Interior to rise to 800m/min from 30m/min, software therefrom averagely takes 50 points to be recorded automatically.There is no sample can be in this experiment
Drafting rate reaches still not broken after 800m/min, therefore experimental endpoints elect silk material breakaway poing as.Drafting force and drafting rate
Relation is shown in Figure 19, the ratio (V of drafting rate and piston speed during fracturehaul-off,break/Vpiston) with composition relation see figure
20, the ratio can show the tensility of sample melt, and the bigger explanation sample of ratio is easily drawn as thinner fiber.Need
Brighter, the fiber of comparative example 1, because itself setting rate is slow, is difficult to after mouth mold extrusion so as to easy to stick on deflector roll
Drawing, therefore the fiber of comparative example 1 is not collected into, this also reflects that CAB addition has substantially for the hardening for accelerating PBAT
Effect, and then improve processability, widen application.For the fiber being collected into, the fiber of embodiment 1 and embodiment 2
Although very thin, its hardening by cooling is still partially slow, has obvious adhesion between the fiber for causing to be collected into, it is difficult to separated
Obtain single fiber.And in following ratio PBAT-CAB：During 20~50%-50~80%, obtained filament silk is clearly demarcated, several
There is no adhesion phenomenon, obtain good technique effect.It can be observed from fig. 19 that drafting force has fluctuated with drafting rate, but
Basic change is little；For drafting force, it can be found that gradually increasing from embodiment 1 to embodiment 5, reach most to comparative example 2
Greatly, show that the drafting force of sample raises with the wherein increase of CAB contents.Figure 20 shows embodiment 1 to embodiment 5
VHaul-off,Break/VPistonNumerical value is gradually reduced, and after great-jump-forward drops to comparative example 2, reaches minimum value, it means that in sample
PBAT presence has better beneficial to increase draftability, PBAT more at most draftabilitys.With reference to result above, we can tentatively obtain
To draw a conclusion：The draftabilitys of PBAT in itself are preferable, but its hardening by cooling is slower, add after CAB (especially when CAB contents reach
During to 50%) can effectively solve this problem, and although CAB has faster setting rate, but the draftability deficiency of itself,
Add PBAT and can effectively improve this problem afterwards.In summary, PBAT and CAB raw materials can effectively improve not by blending
Foot, can obtain not inter-adhesive fine fibre.
【Embodiment 18】
The condition of PBAT/CAP blendings particle also as described above has been subjected to spinning experiment, found because its melt is strong
Compatibility is bad between spending small and component, and silk thread is easily pulled off under relatively low drafting rate, thus be difficult to obtain as
Thin and uniform fiber prepared by PBAT/CAB blending particles.This shows the having using PBAT/CAB as representative that the present invention announces
The thermoplastic cellulose of special rheological behaviour has excellent performance in spinning field with aliphatic aromatic copolyester blends
And application potential.
In shear rate it is 100s at 1 180 DEG C of table-1When actual measurement apparent shear viscosity, theoretical table shear viscosity and two
The difference and difference percentage of person
Actual measurement apparent shear viscosity, theoretical apparent shear viscosity at 2 180 DEG C of table when shear rate is 1363s-1 with
And both differences and difference percentage
The Thermal Parameter for each particle that table 3 is obtained by DSC results.
Table 4 surveys melt index (190 DEG C, 2.16kg) and addition theory melt index and both difference and difference
Percentage
Actual measurement apparent shear viscosity, theoretical table shear viscosity at 5 180 DEG C of table when shear rate is 100s-1 and
Both differences and difference percentage
Actual measurement apparent shear viscosity, theoretical apparent shear viscosity at 6 180 DEG C of table when shear rate is 1000s-1 with
And both differences and difference percentage
Table 7 surveys melt index (190 DEG C, 2.16kg) and addition theory melt index and both difference and difference
Percentage
Claims (10)
1. a kind of thermoplastic cellulose and aliphatic aromatic polyester blending fibres, the blend fibers contain 20% to
The aliphatic aromatic copolyesters of the thermoplastic cellulose of 80% mass and 80% to 20% quality, it is characterised in that the quality
Thermoplastic cellulose and aliphatic aromatic copolyester blends melt viscosity in low shear rate (100s-1) under the conditions of compare
The blending addition theoretical value at least low about 20% of two kinds of initiation materials；In high-rate of shear (1000 or 1363s-1) under the conditions of ratio two
The blending addition theoretical value raw material at least low 20% of kind initiation material；Wherein, the thermoplastic cellulose be selected from cellulose with extremely
The cellulose esters that few two kinds of organic acids are formed, the total number of carbon atoms of the organic acid are more than or equal to 6.
2. according to thermoplastic cellulose and aliphatic aromatic polyester blending fibres described in claim 1, its feature
It is that the substitution value of described thermoplastic cellulose is more than 1.0.
3. according to thermoplastic cellulose and aliphatic aromatic polyester blending fibres described in claim 1, its feature
It is the thermoplastic cellulose for cellulose acetate-butyrate, acetic acid cellulose valerate ester, acetic acid cellulose caproate ester, acetic acid
Enanthic acid cellulose esters, laurate cellulose esters, acetic acid cellulose pelargonate ester, acetic acid capric acid cellulose esters, acetic acid laurate are fine
Tie up plain ester, acetic acid palmitic acid cellulose esters, acetic acid cellulose stearate ester, cellulose propionate butyrate ester, propionic acid cellulose valerate
Ester, propionic acid cellulose caproate ester, propionic acid enanthic acid cellulose esters, propionic acid octanoic acid cellulose esters, propionic acid cellulose pelargonate ester, the propionic acid last of the ten Heavenly stems
At least one in acid cellulose ester, propionic acid laurate cellulose esters, propionic acid palmitic acid cellulose esters, propionic acid cellulose stearate ester
Kind.
4. according to thermoplastic cellulose and aliphatic aromatic polyester blending fibres described in claim 1, its feature
It is that described aliphatic aromatic copolyesters is α, ω-aliphatic diacid or derivatives thereof and aromatic diacid or derivatives thereof
With the copolyesters of aliphatic diol condensation.
5. according to thermoplastic cellulose and aliphatic aromatic polyester blending fibres described in claim 1, its feature
It is containing 2 α to 22 backbone c atoms, ω-aliphatic diacid to be described aliphatic diacid.
6. according to thermoplastic cellulose and aliphatic aromatic polyester blending fibres described in claim 1, its feature
It is that described aliphatic diacid is the aliphatic diacid containing substituent.
7. according to thermoplastic cellulose and aliphatic aromatic polyester blending fibres described in claim 1, its feature
It is that described aliphatic aromatic copolyesters includes the aliphatic aromatic copolyesters by chain extension.
8. according to thermoplastic cellulose and aliphatic aromatic polyester blending fibres described in claim 1, its feature
It is the number-average molecular weight of the blend at least above 20000g/mol, weight average molecular weight is at least above 60000g/mol.
9. according to the thermoplastic cellulose and aliphatic aromatic copolyesters with the special rheological equationm of state described in claim 1
Blend fibers, it is characterised in that the melt index of the blend is at least higher than the blending theory addition value of two kinds of initiation materials
About 10%.
10. a kind of prepare any described thermoplastic cellulose of claim 1~9 and aliphatic aromatic copolyester blends fibre
The method of dimension, using continuous fusion blending extrusion, the desired amount of thermoplastic cellulose and the desired amount of aliphatic aromatic are total to
Polyester is uniformly mixed in the molten state, and is extruded, is granulated；Blends particles are on screw extruder through plastifying, melting
Melt stream is extruded into by spinneret orifice with after metering, through cooling down, stretching the obtained thermoplastic cellulose and aliphatic virtue
Fragrant race's polyester blending fibres.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610803924.4A CN107794593B (en) | 2016-09-06 | 2016-09-06 | Thermoplastic cellulose and aliphatic aromatic copolyester blend fiber and preparation method thereof |
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| WO2023032763A1 (en) * | 2021-08-30 | 2023-03-09 | 旭化成株式会社 | Biodegradable nonwoven fabric and use of same |
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| US20250075031A1 (en) * | 2023-09-05 | 2025-03-06 | Sk Leaveo Co., Ltd. | Eco-friendly biodegradable resin composition and biodegradable nonwoven fabric |
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| CN1183429A (en) * | 1990-11-30 | 1998-06-03 | 伊斯曼化学公司 | Blends of cellulose esters and aliphatic-aromatic copolyesters |
| CN1429290A (en) * | 2000-05-12 | 2003-07-09 | 伊斯曼化学公司 | Copolyesters and fibrous materials formed therefrom |
| CN101142255A (en) * | 2005-03-18 | 2008-03-12 | 诺瓦蒙特股份公司 | Biodegradable aliphatic -aromatic polyesters |
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| CN1183429A (en) * | 1990-11-30 | 1998-06-03 | 伊斯曼化学公司 | Blends of cellulose esters and aliphatic-aromatic copolyesters |
| CN1429290A (en) * | 2000-05-12 | 2003-07-09 | 伊斯曼化学公司 | Copolyesters and fibrous materials formed therefrom |
| CN101142255A (en) * | 2005-03-18 | 2008-03-12 | 诺瓦蒙特股份公司 | Biodegradable aliphatic -aromatic polyesters |
| US8193301B2 (en) * | 2005-03-18 | 2012-06-05 | Novamont S.P.A. | Biodegradable aliphatic-aromatic polyester |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| WO2023032763A1 (en) * | 2021-08-30 | 2023-03-09 | 旭化成株式会社 | Biodegradable nonwoven fabric and use of same |
| JPWO2023032763A1 (en) * | 2021-08-30 | 2023-03-09 | ||
| JP7745639B2 (en) | 2021-08-30 | 2025-09-29 | エム・エーライフマテリアルズ株式会社 | Biodegradable nonwoven fabric and its uses |
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